Lauren Cotten
MENG3316
9
Assignment
MH
K
meanvelooity.am
Um go ul r rdr
fo
Um
fi2ft
Y
fo o if
J
IT
0.2ft
r dr
fo fo r fo
I
0.05ms
dr
MeanTemperature
new
fmr fov Tr dr
Tm
op r
foo I f
Tm fol fo344.8k 344.8
ro
tf
Tm
ftp.f
3442.8
Tm 4 344.8
Z
3
344.8 t
4
Tm 366.67K
t 75
4
3444.8
EE
t
3
3448 75
75yes5 18.8
7,34
trys
4
tf 4
71 71 18.1 t 18.82
4
6
Ea 18.84
6
8
6
t
18.8
fo
rft
7
dr
6
8
18
68 4 t 18g
366.67K
dr
8
6
Tubb
Air
Tmi 75C
Assuming constantSurfall
Temperature
Re
Ac
YpYf z
Re
m 0.001kgIs
ITI
to
350k
V UzPz
300K
V_20.92 15.89 10 6
208.2 184.6 107
µ 0.700
Pi
911
ITDµ TIO
Pr
407
Homem 1.821106MYS
Re 214942300 laminar
III
pressure
03M1197.45611107N4m2Yoann 18.203840
0.707
Cp 1.009 1.007 kJkgk
0.9950 1.1614kg1m3
p
pioatm ppiatm.IO l085kgm3 Interpolated
fam O05ReDPr
g38fYjHnmYsm
ftp
f
Roam 10.085191M
Pr 0.70378
Le1.05REPAID
051214911070378110.03mi
2.27M ThermalEntry
v
fullydeveloped
Length
FEFmm.in
P ITD110.03M
As
Viscosity is inversely proportional
410.001kgIs
4mi
323k
Ts 25 C
Pio10.085kglM3
PAC PITD2
PITDM
P 10Atm
1.82110 6mys
vm ni in4
Re p4tIpj4nip
13 0.03
f Son
Tm 25275 5000
Cp 1.00792kJlkgK
exit
p
I.oqskg1m3
exPlPmfphlxl
IEIHH exptoitoikgmisY.infoaEEiYgkmYY
Tm 34.38 C
qoonvi.MG
Ofcom
outlettemperature
DTi Ts Tmi 25 754 150300 223k
ATO Ts Tmo 25 34.384 1 9.38700 263,621
DTi DTo7 O00lkglsll0O7.92JIkgHl223 263.62k
40.94W
40.94WClearing the flow
A Dp't B
pig Dp f Pyg N X
A0.4581 0 gqlgsmz Dp 0.029t8f10.85kglm3
1 jo
power 4.22405kg_M2
53
5
Power 4.22110 W
210.03M
Dp 0.458Kglms
Dp 0.458Pa
FullyDeveloped laminarflow
64 26,449 0.02978
f
RED
4mk5gfgm
Um hiya
0.001141514
10.85kgtmall.BA
Um 0.1304ms
fluidwater
M 0.02kgIS
T.iq
1
7NYYTs
voom
30
H
1
Re 4in
TDM
Re 410.02kg
am
Utd
OD5RenPr
0.05114038
Xfd8.74M
30 2500 2984
204
water 29800
K
Cp 418051kg
6 NSm2
pipe
TD44
AfITD
0.609Wlmk
Pr 6.225
Is
6225110.02M
laminar
90740
µ
K
NO02M 074106 Ngm2
Re 1403.8
XD
Tm
p 998kgm3
m Qp
0.021415
Q
iy
0
998kgIm's
2.00411051m31s
A OYA 2.0041109M2
17410.0212
I
0.06379ms
V
V
y
9071106 NS
m2
998141ms
9.091107 MYS
A151316
Di 0.02M
Do_0.04M
f ITD
f Ilroi ri
f 1174 Doe Dill
W6WM3
0.1kgIs
1
1
1
Tmi Lola
30
1
TmL024000
410.1kgIs
Re 4mi
111
IDM ICU02M 81271106Nsm2
Tm 303k
Re 7840 turbulent
WATER
Iq
1 1 11
Tmo 40 i
I
r
er
l
Cp 417951kgk
8121106 NSm2
µ
12 0.617WINK
il l l
Idf
p
i
Pr 5.52
Abl 316 Steel
T 400k
12 15.2
o
0.02M
Xtd
Dilturb N
o
ovum
504
01M
Eg Ofcom
F 300k
13.4 WINK
468TlkgK
Interpolated
k 13.45WINK
p
McplTmo Tmi
n303k
469.0851kgK
8238kgIm
Cft
MlpTmo Tmi_qIlDo2 Di'll
4
0.1kg1514179 51kg4 Lok
106WIM
L 8.87M
4
0.0420.0271
fully developed turbulent flow w Smooth Surfaces
No0.023Re Pr
Nu
N 0.4 for heating
0.0231784070815.52104
Nu 59.42
NT HI
Kt
s
59.42
5 10.04M
0.617W
lmk
A 117410.042 0.022
A 11740.0012
sh 1833.21WINK
dfsAs mcplTs Tmo
ts
sttm.o
iffyn
Ts42.26
106wlm3LTHKO042O.IM
0.119151417951kgK
t3l3K 315.26k